AU5400896A - Mixing - Google Patents
MixingInfo
- Publication number
- AU5400896A AU5400896A AU54008/96A AU5400896A AU5400896A AU 5400896 A AU5400896 A AU 5400896A AU 54008/96 A AU54008/96 A AU 54008/96A AU 5400896 A AU5400896 A AU 5400896A AU 5400896 A AU5400896 A AU 5400896A
- Authority
- AU
- Australia
- Prior art keywords
- mixing
- gas
- liquid
- nozzle opening
- cross
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Water Treatments (AREA)
- Led Devices (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Description
MIXING
FIELD OF TECHNOLOGY
The invention pertains to the field of process technology and relates to an apparatus and method for mixing a gas with a liquid. The invention can be used, for example, in ore dressing, in dissolving processes, and in the aeration of water.
BACKGROUND
For the mixing of a gas with a liquid there are used, for example, perforated nozzles through the perforations of which the gas is directed under pressure into the liquid.
Figure 5 in publication GB-1115288 also shows a mixing ap¬ paratus in which into a space between two cylindrical surfaces there are fed tangentially a liquid into the upper section and a gas at a lower point, under an annular skirt. The mixture is withdrawn upwards via a connection in the center. In this appa¬ ratus, the cross-sectional area of the opening which leads out of the annular mixing space is greater than the area of the feed connections.
DESCRIPTION OF THE INVENTION
General description
A mixing apparatus according to Claim 1 has now been invented. Certain preferred embodiments of the invention are stated in the other claims.
The most essential idea of the invention is that the liquid and the gas to be mixed with it are fed tangentially into the space between two surfaces of revolution so that the mixture comes into a rotary motion in the space, and that the mixture leaves the mixing space via a nozzle opening the cross-sectional area of which is smaller than the cross-sectional area of the feed connections. During the rotary motion the gas will both become mixed in the form of small bubbles with the liquid and dissolve in the liquid. Preferably the pressure in the mixing space is higher than after the nozzle opening, so that after the mixing space the liquid will be supersaturated. In this case, gas will separate from the solution and micro-sized gas bubbles will form.
The nozzle opening is preferably at one end of the mixing space.
There may be even a plurality of feed connections, and they may be placed at desired locations either on the outer or on the inner periphery of the mixing space.
The shape of the reactor may vary, and it is determined accord¬ ing to the use and the application.
The invention can be used, for example, in froth flotation of ores for the forming of bubbles and for the maintaining of a slurry suspension. The invention is highly applicable also to the aeration of waste water tanks and watercourses. Various dissolving processes requiring the adding of a gas are also typical areas of use for the invention.
Description of the drawings
In the drawings of the specification, Figure 1 shows a top view of a gas-mixing reactor according to the invention, and Figure
2 shows a side view of the same apparatus, in section through A-A, and Figure 3 shows a froth flotation apparatus in which mixing according to the invention is used.
Detailed description of certain embodiments
The reactor shown in Figures 1 and 2 has a cylindrical outer mantle 1 and, inside it parallelly, a narrower inner mantle 2, which is attached to the closed upper end 3 of the reactor but detached from the reactor bottom 4. Between the mantles there is left an annular chamber 5. There is an opening 6 in the center of the reactor bottom.
The inner mantle 2 has here a cylindrical narrower upper sec¬ tion and a broader cylindrical lower section linked thereto via a conical intermediate section. Thus the cross-sectional area of the upper section of the reactor is greater.
At the upper end of the annular chamber 5 the outer mantle 1 has a feed inlet 7 and in it tangentially a feed pipe 8. A liquid material and a gas to be incorporated into it are fed under pressure via the feed pipe into the annular chamber in such a manner that they come into a rotary motion in the an¬ nular chamber. Gas is incorporated, both as bubbles and dis¬ solved, into the liquid. Any gas not mixed with the liquid separates as a ring on the surface of the inner mantle. From this, gas becomes further mixed into the liquid.
At the bottom 4 of the reactor, in its corner, there is an an¬ nular limiting ring 9 in such a manner that, between the lower end of the inner mantle 2 and the limiting ring, there is formed an annular nozzle opening 10 having a flow cross section smaller than the cross section of the upstream part of the annular chamber.
The reactor is operated at such a feed pressure that, when the mixture flows to the nozzle opening 10 and its pressure de¬ creases, the mixture is supersaturated with respect to gas, in which case dissolved gas separates out, forming micro-sized bubbles. Such micro-bubbles adhere to the surfaces of larger bubbles in the mixture. These larger bubbles serve as efficient carrier bubbles. Owing to the micro-bubbles the total surface area of the bubbles is very large. The size, number and mutual proportions of the bubbles can be adjusted by adjusting the feed ratio, feeding pressure, or the surface area of the nozzle opening.
The upper end of the inner mantle 2 may also be open, in which case bubbles will leave via that route. Such an apparatus would be especially suited for the processing of a slurry, in which case heavier slurry will leave via opening 6.
The mineral slurry froth-flotation apparatus according to Fig¬ ure 3 has a container 11 and, inside it, a gas-mixing reactor 12 of the type described above. Slurry is introduced into the container from the upper end via a feed pipe 13. At the lowest point of the reactor bottom 14 there is connected a recycling pipe 15, through which slurry which has settled on the bottom is directed by means of a pump 16 to the feed pipe 8 of the mixing reactor. Air via connection 17 is also fed into the feed pipe. The overpressure prevailing in the feed pipe is, for example, 1-2 bar. In the reactor, air becomes mixed with the slurry and partly dissolved therein. A large quantity of micro- bubbles are formed in the mixture emerging from the reactor. Hydrophobic mineral particles from the slurry adhere to the surfaces of the bubbles. The bubbles rise to the surface of the container as a froth, which is recovered for further treatment. The process is dimensioned so that the bubbles will have time to separate from the slurry as completely as possible before the slurry flows into the recycling pipe.
Claims (6)
1. An apparatus for mixing a gas with a liquid, which ap¬ paratus has a mixing chamber, at least one feed connection for feeding the gas and the liquid tangentially as a continuous stream into the chamber, and a nozzle opening for withdrawing the mixture as a continuous stream from the mixing chamber, characterized in that the mixing chamber has a mixing space (5) between two surfaces of revolution one inside the other, into which space the feed connections (8) lead tangentially, and that the cross-sectional area of the nozzle opening (10) is smaller than the cross-sectional area of the feed connections.
2. An apparatus according to Claim 1, characterized in that the cross-sectional area of the mixing chamber (5) at a point before the nozzle opening (10) is larger than the cross- sectional area of the nozzle opening.
3. An apparatus according to Claim 1 or 2, characterized in that the nozzle opening (10) is at one end of the mixing space (5).
4. An apparatus according to Claim 3, characterized in that the nozzle opening (10) is annular.
5. A method for mixing a gas with a liquid, in which method the gas and the liquid are introduced as a continuous stream via feed connections into a mixing chamber, and the mixture of gas and liquid is withdrawn as a continuous stream from the mixing chamber, characterized in that the gas and the liquid are fed into the mixing chamber, which is a mixing space be¬ tween two surfaces of revolution one inside the other, tangen¬ tially so that the mixture comes into a rotary motion around the mixing space and that the mixture is withdrawn from the mixing space via a nozzle opening having a cross-sectional area smaller than the cross sectional area of the feed connections.
6. A froth-flotation process or a dissolving process, charac¬ terized in that it uses an apparatus according to any of Claims 1-4 or a method according to Claim 5.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI951881A FI98053C (en) | 1995-04-20 | 1995-04-20 | Blend |
FI951881 | 1995-04-20 | ||
PCT/FI1996/000215 WO1996033006A1 (en) | 1995-04-20 | 1996-04-19 | Mixing |
Publications (2)
Publication Number | Publication Date |
---|---|
AU5400896A true AU5400896A (en) | 1996-11-07 |
AU700212B2 AU700212B2 (en) | 1998-12-24 |
Family
ID=8543272
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU54008/96A Ceased AU700212B2 (en) | 1995-04-20 | 1996-04-19 | Mixing |
Country Status (9)
Country | Link |
---|---|
US (1) | US6019497A (en) |
EP (1) | EP0822858B1 (en) |
AU (1) | AU700212B2 (en) |
CA (1) | CA2221714A1 (en) |
DE (1) | DE69621795T2 (en) |
ES (1) | ES2177778T3 (en) |
FI (1) | FI98053C (en) |
PT (1) | PT822858E (en) |
WO (1) | WO1996033006A1 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AUPO887597A0 (en) * | 1997-08-29 | 1997-09-25 | Separation Technologies Group Pty Ltd | Mixing apparatus |
WO2008127533A1 (en) * | 2007-04-13 | 2008-10-23 | Freeman Energy Corporation | Biomass cultivation system and corresponding method of operation |
JPWO2018190298A1 (en) * | 2017-04-10 | 2020-02-20 | オオノ開發株式会社 | Stirring vessel, mixing device, and method for producing mixed fluid |
Family Cites Families (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL75043C (en) * | 1951-11-30 | |||
US3131037A (en) * | 1959-06-29 | 1964-04-28 | Stora Kopparbergs Bergslags Ab | Oil gasifier |
GB1115288A (en) * | 1965-06-14 | 1968-05-29 | Equipment Engineers Inc | Methods and apparatus for effecting dispersions of gas in liquid materials |
US3775314A (en) * | 1971-06-07 | 1973-11-27 | Water Treatment Corp | Method and apparatus for mixing gases with water |
JPS5117145B2 (en) * | 1971-09-10 | 1976-05-31 | ||
US4014961A (en) * | 1973-04-24 | 1977-03-29 | Vitaly Fedorovich Popov | Ejector mixer for gases and/or liquids |
SU685806A1 (en) * | 1978-05-31 | 1979-09-15 | Всесоюзный Ордена Трудового Красного Знамени Научно-Исследовательский Институт Буровой Техники | Apparatus for preparing aerated drilling and cementing muds |
US4215081A (en) * | 1979-01-24 | 1980-07-29 | Brooks Kirtland H | Liquid aerator |
US4415275A (en) * | 1981-12-21 | 1983-11-15 | Dietrich David E | Swirl mixing device |
US4398827A (en) * | 1980-11-10 | 1983-08-16 | Dietrich David E | Swirl mixing device |
JPS6038028A (en) * | 1983-08-08 | 1985-02-27 | Isobe Shigeo | Instantaneous mixing method of particulate material and liquid |
FR2587915B1 (en) * | 1985-09-27 | 1987-11-27 | Omya Sa | DEVICE FOR CONTACTING FLUIDS IN THE FORM OF DIFFERENT PHASES |
US4688945A (en) * | 1985-10-02 | 1987-08-25 | Stranco, Inc. | Mixing apparatus |
CA2114294A1 (en) * | 1993-01-05 | 1995-07-27 | Thomas Earle Allen | Apparatus and method for continuously mixing fluids |
SE504247C2 (en) * | 1994-03-24 | 1996-12-16 | Gaevle Galvan Tryckkaerl Ab | Vessels for treating fluid |
-
1995
- 1995-04-20 FI FI951881A patent/FI98053C/en active IP Right Grant
- 1995-08-03 US US08/930,711 patent/US6019497A/en not_active Expired - Fee Related
-
1996
- 1996-04-19 CA CA002221714A patent/CA2221714A1/en not_active Abandoned
- 1996-04-19 DE DE69621795T patent/DE69621795T2/en not_active Expired - Fee Related
- 1996-04-19 WO PCT/FI1996/000215 patent/WO1996033006A1/en active IP Right Grant
- 1996-04-19 PT PT96910983T patent/PT822858E/en unknown
- 1996-04-19 AU AU54008/96A patent/AU700212B2/en not_active Ceased
- 1996-04-19 ES ES96910983T patent/ES2177778T3/en not_active Expired - Lifetime
- 1996-04-19 EP EP96910983A patent/EP0822858B1/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
EP0822858A1 (en) | 1998-02-11 |
FI98053B (en) | 1996-12-31 |
AU700212B2 (en) | 1998-12-24 |
DE69621795T2 (en) | 2003-02-20 |
DE69621795D1 (en) | 2002-07-18 |
CA2221714A1 (en) | 1996-10-24 |
EP0822858B1 (en) | 2002-06-12 |
FI98053C (en) | 1997-04-10 |
WO1996033006A1 (en) | 1996-10-24 |
PT822858E (en) | 2002-11-29 |
ES2177778T3 (en) | 2002-12-16 |
FI951881A (en) | 1996-10-21 |
FI951881A0 (en) | 1995-04-20 |
US6019497A (en) | 2000-02-01 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
MK14 | Patent ceased section 143(a) (annual fees not paid) or expired |